KR960022425A - 파라포름알데히드 제조방법 - Google Patents

파라포름알데히드 제조방법 Download PDF

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KR960022425A
KR960022425A KR1019950020901A KR19950020901A KR960022425A KR 960022425 A KR960022425 A KR 960022425A KR 1019950020901 A KR1019950020901 A KR 1019950020901A KR 19950020901 A KR19950020901 A KR 19950020901A KR 960022425 A KR960022425 A KR 960022425A
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amine
zone
catalyst
temperature
homogenized mixture
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KR100249275B1 (ko
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이크-반셀스 루이스
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안젤 수로카 수로카
패텐테스 오이 노베다데스, 에스. 엘
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/02Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
    • C07C47/04Formaldehyde
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2/00Addition polymers of aldehydes or cyclic oligomers thereof or of ketones; Addition copolymers thereof with less than 50 molar percent of other substances
    • C08G2/08Polymerisation of formaldehyde

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Saccharide Compounds (AREA)
  • Catalysts (AREA)
  • Phenolic Resins Or Amino Resins (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Cosmetics (AREA)

Abstract

본 발명의 방법은 80 내지 89% 농도의 포름알데히드 용액을 공급하는 단계; 용액을 80 내지 100℃로 가열하는 단계; 가열된 용액을 가열된 영역에서부터 다른 냉각된 영역으로 이동하는 금속 벨트 콘베이어의 가열된 영역에 유출하는 단계를 포함한다. 바람직하기로는, 포름알데히드 용액이 미리 촉매와 혼합된다.

Description

파라포름알데히드 제조방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (11)

  1. 80 내지 89wt%의 순도를 갖는 파라포름알데히드의 연속 제조방법에 있어서, 원하는 파라포름알데히드와 실질적으로 동일한 순도의 포름알데히드 용액을 공급하는 단계; 상기 용액을 80 내지 100℃의 온도로 가열하는 단계; 상기 가열된 용액을 제1의 가열영역에서 제2냉각영역들로 이동하는 금속 콘베이어 벨트위로 유출되며, 상기 유출이 상기 제1영역의 한 영역상에서 이루어지는 단계를 포함하는 것을 특징으로 하는 제조방법.
  2. 제1항에 있어서, 상기 포름알데히드 용액을 믹서에 넣은 다음 촉매를 가하는 단계; 상기 포름알데히드 용액과 상기 촉매가 균질화된 혼합물이 얻어질 때까지 80 내지 100℃의 온도에서 혼합되는 단계; 상기 온도 범위를 유지하면서 상기 균질화된 혼합물이 상기 금속 벨트 콘베이어의 상기 제1영역위로 유출되는 단계를 포함하는 것을 특징으로 하는 방법.
  3. 제2항에 있어서, 상기 촉매가 강알칼리성 수산화물인 것을 특징으로 하는 방법.
  4. 제2항에 있어서, 상기 촉매가 pKa값이 10.4 내지 11.3인 아민인 것을 특징으로 하는 방법.
  5. 제4항에 있어서, 상기 아민이 메틸아민, 에틸아민, n-프로필아민, n-부틸아민, 이소-부틸아민 및 터트-부틸아민으로 이루어진 군으로부터 선택되는 일차아민인 것을 특징으로 하는 방법.
  6. 제4항에 있어서, 상기 아민이 디메틸아미, 디에틸아민, 디-n-프로필아민, 디-이소-프로필아민 및 디부틸아민으로 이루어진 군으로부터 선택되는 이차아민인 것을 특징으로 하는 방법.
  7. 제4항에 있어서, 상기 아민이 트라에틸아민, 트리에탄올아민으로 이루어진 군으로부터 선택되는 삼차아민인 것을 특징으로 하는 방법.
  8. 제4항 내지 제7항 중 어느 한 항에 어서, 상기 균질화된 혼합물의 아민 농도 00000가 6.0 내지 20,0meq/㎏인 것을 특징으로 하는 방법.
  9. 제8항에 있어서, 상기 균질화된 혼합물에서 아민 농도가 약 9.5meq/㎏인 것을 특징으로 하는 방법.
  10. 제1항 내지 제9항 중 어느 한 항에 있어서, 상기 제1영역의 온도가 70 내지 90℃로 유지되는 것을 특징으로 하는 방법.
  11. 제1항 내지 제9항 중 어느 한 항에 있어서, 상기 제2영역의 온도가 25 내지 35℃로 유지되는 것을 특징으로 하는 방법.
    ※ 참고사항:최초출원 내용에 의하여 공개하는 것임.
KR1019950020901A 1994-12-09 1995-07-15 파라포름알데히드 제조방법 Expired - Fee Related KR100249275B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ES9402512 1994-12-09
ES09402512A ES2087041B1 (es) 1994-12-09 1994-12-09 Procedimiento para la preparacion de paraformaldehido.

Publications (2)

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KR960022425A true KR960022425A (ko) 1996-07-18
KR100249275B1 KR100249275B1 (ko) 2000-03-15

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KR1019950020901A Expired - Fee Related KR100249275B1 (ko) 1994-12-09 1995-07-15 파라포름알데히드 제조방법

Country Status (29)

Country Link
US (1) US5686554A (ko)
EP (1) EP0716104B1 (ko)
JP (1) JP2796669B2 (ko)
KR (1) KR100249275B1 (ko)
CN (1) CN1061641C (ko)
AT (1) ATE193308T1 (ko)
AU (1) AU695649B2 (ko)
CA (1) CA2153452C (ko)
CZ (1) CZ288105B6 (ko)
DE (1) DE69517138T2 (ko)
EE (1) EE03254B1 (ko)
ES (1) ES2087041B1 (ko)
FI (1) FI113780B (ko)
GR (1) GR3034085T3 (ko)
HR (1) HRP950396B1 (ko)
HU (1) HU214094B (ko)
MX (1) MX192468A (ko)
NO (1) NO307383B1 (ko)
NZ (1) NZ272534A (ko)
PL (1) PL179331B1 (ko)
PT (1) PT716104E (ko)
RU (1) RU2148592C1 (ko)
SA (1) SA95160120B1 (ko)
SG (1) SG33401A1 (ko)
TH (1) TH12621A (ko)
TW (1) TW285666B (ko)
UA (1) UA44697C2 (ko)
VN (1) VN498A1 (ko)
YU (1) YU48905B (ko)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2153661T3 (es) * 1996-03-20 2001-03-01 Celanese Int Corp Adicion de amina para mejorar paraformaldehido.

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3001235A (en) * 1958-07-26 1961-09-26 Sumitomo Chemical Co Method for the manufacture of a formaldehyde polymer in a crape-chip form
US2992277A (en) 1959-04-28 1961-07-11 Du Pont Paraformaldehyde manufacture
ES341724A1 (es) * 1967-06-13 1968-10-01 Ordieres Perfeccionamientos introducidos en los procedimientos de polimerizacion de soluciones de formaldehido.
FR1547172A (fr) * 1967-07-17 1968-11-22 Sir Soc Italiana Resine Spa Procédé de production du paraformaldéhyde
FR2067169A1 (en) * 1969-11-19 1971-08-20 Charbonnages Ste Chimique Paraformaldehyde from aq formaldehyde
US4277402A (en) * 1979-07-03 1981-07-07 Nasa Synthesis of polyformals
US4550213A (en) 1984-06-29 1985-10-29 Celanese Corporation Method of manufacture for paraformaldehyde prills
DD272576A3 (de) * 1987-01-30 1989-10-18 Leuna Werke Veb Verfahren zur herstellung von koernigem paraformaldehyd
DE3925966A1 (de) 1989-08-05 1991-02-07 Leuna Werke Veb Lp 86 148 - verfahren zur herstellung von koernigem paraformaldehyd
CN1029351C (zh) 1989-09-16 1995-07-19 陈方 高甲醛含量的多聚甲醛的制造方法
US5302277A (en) * 1990-11-28 1994-04-12 Mitsui Toatsu Chemicals, Incorporated Process for producing paraformaldehyde of high formaldehyde content

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Publication number Publication date
CN1124242A (zh) 1996-06-12
DE69517138T2 (de) 2001-02-01
US5686554A (en) 1997-11-11
HU214094B (en) 1997-12-29
MX192468A (es) 1999-06-24
HUT75584A (en) 1997-05-28
VN498A1 (ko) 1998-05-25
GR3034085T3 (en) 2000-11-30
CA2153452C (en) 2006-08-29
FI113780B (fi) 2004-06-15
NO952691L (no) 1996-06-10
ES2087041B1 (es) 1997-03-16
DE69517138D1 (de) 2000-06-29
HRP950396A2 (en) 1997-10-31
HRP950396B1 (en) 2001-02-28
JP2796669B2 (ja) 1998-09-10
CZ288105B6 (cs) 2001-04-11
YU48905B (sh) 2002-10-18
AU2496095A (en) 1996-06-20
TH12621A (th) 1996-09-10
CZ243995A3 (en) 1996-06-12
NO307383B1 (no) 2000-03-27
NO952691D0 (no) 1995-07-06
PL310573A1 (en) 1996-06-10
SG33401A1 (en) 1996-10-18
CA2153452A1 (en) 1996-06-10
FI953683A0 (fi) 1995-08-02
EE03254B1 (et) 2000-02-15
UA44697C2 (uk) 2002-03-15
NZ272534A (en) 1996-03-26
HU9502048D0 (en) 1995-09-28
PL179331B1 (pl) 2000-08-31
RU2148592C1 (ru) 2000-05-10
TW285666B (ko) 1996-09-11
MX192468B (ko) 2016-01-29
PT716104E (pt) 2000-11-30
ATE193308T1 (de) 2000-06-15
ES2087041A1 (es) 1996-07-01
SA95160120B1 (ar) 2005-05-16
AU695649B2 (en) 1998-08-20
EP0716104A1 (en) 1996-06-12
FI953683L (fi) 1996-06-10
EP0716104B1 (en) 2000-05-24
JPH08165262A (ja) 1996-06-25
YU54395A (sh) 1997-12-05
CN1061641C (zh) 2001-02-07
KR100249275B1 (ko) 2000-03-15

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